Method for producing solid urea by granulation

ABSTRACT

Method for producing solid urea by granulation, wherein the granulation is fed with liquid urea having a purity greater than 98% by weight and not containing formaldehyde.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application is a continuation of U.S. patent application Ser. No.15/741,652, filed Jan. 3, 2018, which is a national phase ofPCT/EP2016/063027, filed Jun. 8, 2016, and claims priority to EuropeanPatent Application No. 15175347.2, filed Jul. 3, 2015, the entirecontents of all of which are incorporated herein by reference.

FIELD OF APPLICATION

The invention relates to the field of the production of solid urea.

PRIOR ART

Solid urea is produced mainly by prilling or granulation.

Prilling involves cooling droplets of liquid urea falling inside a towerby means of counter-flowing air. The solids thus formed are termedprills. Granulation involves spraying liquid urea onto granules inside aproper granulator, for example in a fluid bed; the liquid forms a layerwhich solidifies, thus increasing the size of the granule. Bothtechniques are known to persons skilled in the art and are described inthe literature, for example in Meessen, “Urea”, Ullmann's Encyclopediaof Industrial Chemistry, Wiley-VCH Verlag, 2010.

Granulation offers a series of recognized advantages and is consideredto be superior to prilling. It is well-known that the prills have acertain fragility essentially due to the rapid cooling of the dropletswhich creates a porous structure. The solid product obtained bygranulation has a much greater mechanical strength, in particularagainst crushing and knocks, and is therefore more suitable for storageand transportation in bulk form. Another advantage of granulation is thecapacity to produce granules of a larger size, for example with adiameter of 3 mm or more, while the diameter of prills is no more than 2mm because larger dimensions would require a too large and expensiveprilling tower and would originate problems of instability of thedroplets.

Despite these advantages, however, most of the solid urea is nowadaysproduced using the prilling technique owing to the lower cost of aprilling section compared to a granulation section.

According to the prior art and the technical literature, a prillingprocess requires a urea melt with a high concentration, preferably witha concentration of 99.7% by weight or more. As known, the urea plantsproduce (downstream of the recovery section) a solution containing acertain quantity of water (typically about 30%); hence the aforesaidconcentration is reached using a suitable concentration and evaporationsection designed to completely remove the water.

A granulation process, instead, according to the teaching of the priorart, is carried out with a solution of urea having a concentration of96% or up to a maximum of 98% by weight, i.e. still containing about2-4% of water. The granulation process is regarded as being able totolerate a greater water content than prilling and therefore the priorart does not consider it necessary to entirely remove the water.Furthermore, a water content of around 4% is considered advantageous inthe granulation process to avoid the formation of biuret which is anundesirable by-product.

The suppliers of urea technologies have developed specific granulationtechnologies which differ as regards certain details, but have in commonthe fact that they use urea with the abovementioned concentration level.

Another characteristic of the known processes—both granulation andprilling—is the addition of formaldehyde as additive for improving themechanical characteristics of solid urea. Typically, formaldehyde isadded in quantities of between 0.2% and 0.4% of the urea. The additionof formaldehyde is considered indispensable for facilitating granulationand for obtaining the mechanical strength required by the market,although it involves two drawbacks.

A first drawback is the cost: plants which produce thousands of tons ofurea per day require a large quantity of formaldehyde, of the order ofseveral tons per day, which must be provided. Formaldehyde is not alwaysproduced on site and many urea plants are located in remote areas.Providing this additive therefore gives rise to a high purchase,transportation and storage cost.

Another drawback, which is receiving an increasing attention, is theenvironmental impact. Solid urea (prills or granules) is mainly used inagriculture as fertilizer, which means that the formaldehyde containedin the urea is released into the ground. This creates a negative impacton the environment and problems for the human health, since formaldehydeis considered a possible carcinogen agent. But nevertheless, it isconsidered to be indispensable. There are procedures for producing ureawithout formaldehyde (called “technical urea”) which, however, arecostly and produce small amounts.

For the above reasons, it can be understood that there is a need toimprove the quality of solid urea, in particular with reference to itspurity and mechanical strength.

SUMMARY OF THE INVENTION

The idea forming the basis of the invention is to use a pure urea meltin a granulation process, without the addition of formaldehyde.

Advantageously, said urea melt has a purity of more than 98% by weight,more advantageously of at least 99.5% and even more advantageously of atleast 99.7%.

The applicant has found that in conventional granulation processes thewater contained in the urea feed, although in small amounts (approx.3-4%), worsens the quality of the product. Granulation is essentially alayer-by-layer growth process and the applicant has noted thatevaporation of the water (which occurs during granulation) tends togenerate porosity within the core of the granule. Therefore, althoughthe surface, i.e. the outer layer, appears to have good visual andmechanical properties, the internal layers of the granule are weakenedby the porosity.

This technical problem has never been recognized in the prior art, whichon the contrary encourages granulation with a urea feed of around 96% byweight. The applicant has found that a granulation process starting fromsubstantially anhydrous urea (concentration of more than 98%) achieves amechanical quality such that the addition of formaldehyde is no longerrequired. The applicant has also found that the formation of biuretnevertheless remains within the standard levels accepted by the market(for example less than 0.9%).

It should be noted that the invention requires to remove water in a moreefficient way compared to conventional granulation technology, and thismay result in an—albeit limited—additional cost. This cost is howeveroffset by the superior quality of the end product and in particular bythe huge advantage represented by the elimination of added formaldehyde.

The superior quality of the product arises from the improved granulestructure. The invention allows obtain a more uniform granule structureowing to the elimination of the water evaporation generating porosity inthe internal layers of the granule.

The elimination of the formaldehyde gives rise to dual benefit becauseit eliminates a costly item and a source of concern in terms ofecological and environmental impact.

The invention provides a technique for obtaining solid urea in granuleform which is free from formaldehyde. The invention therefore enablesurea producers to provide a product which has a mechanical strengthequivalent to or superior to the granules which are nowadays available,but has the advantage of containing no formaldehyde and of beingregarded as an environmentally friendly product. Formaldehyde-free ureais thus available at lower costs compared to the known processes for theproduction of technical urea.

An aspect of the invention is also a method for revamping existingplants with a prilling section. These plants already have an evaporationsection designed to reach a high concentration (e.g. 99.7%) for correctfeeding of the prilling tower, and therefore may be revamped by adding agranulation section and feeding at least part of the high-concentrationurea melt, which is provided by the existing evaporation section, to thenew granulation section. By doing so, the plant provides an improvedproduct (granules instead of prills), the addition of formaldehyde canbe eliminated and the already present evaporation section is exploited.

In this way the invention also responds to the need of revamping andimproving the prilling tower-based urea plants, which are oftenoutdated, but are still present in large numbers all over the world.

According to an embodiment of the invention, a part of the urea melt canbe used in a prilling tower to produce seeds for the granulationprocess. This process is advantageous particularly when the invention isapplied to the revamping of a urea plant comprising a prilling tower,since the existing prilling tower can be used for said purpose. In someembodiments the production of prills can be discontinued, which meansthat the output of the revamped plant is solely of granules.

The invention can be implemented using all the granulation techniquesknown per se. Preferably, fluid-bed granulation can be used. Even morepreferably, fluid-bed granulation inside a longitudinal granulator maybe used, where the fluidized granules rotate to form a vortex or twocounter-rotating vortices, as explained for example in EP 1412069. Partof the urea melt feed may be suitably used to produce the seeds of thegranulation process.

DESCRIPTION OF THE FIGURES

FIG. 1 is a scheme of a first embodiment of the invention.

FIG. 2 is a scheme of a second embodiment.

FIG. 3 is a scheme of a third embodiment.

DESCRIPTION OF PREFERRED EMBODIMENTS

FIG. 1 shows a schematic urea plant comprising a synthesis section USand a recycling section UR. The recycling section UR provides an aqueoussolution of urea SOL containing about 70% by weight of urea.

Said solution passes through evaporation section EV inside which thewater is removed, obtaining a urea melt UM containing more than 98%, forexample 99.7%, by weight of urea. Said urea melt UM, without theaddition of formaldehyde, is fed to a granulation section GS, obtaininggranules of urea U.

FIG. 2 shows an example of revamping of a plant in which the urea meltUM is originally fed to a prilling section PS which produces urea prillsP. At least a part UM′ of said urea melt UM is fed to a granulationsection GS which is arranged parallel to the prilling section PS, alsoin this case without the addition of formaldehyde.

In some embodiments, the UM stream is directed entirely towards the newgranulation section GS, i.e. the production of prills P is discontinued.

FIG. 3 illustrates an embodiment which is a variant of FIG. 2, wherein aportion UM″ of the urea melt is used in the existing prilling section PSto produce solid seeds S for the granulation section GS.

1. A method for producing solid urea by granulation, wherein thegranulation is fed with a urea melt having a concentration of more than98% by weight and no formaldehyde is added to said urea melt.
 2. Themethod according to claim 1, wherein said urea melt has a concentrationof at least 99.5% by weight.
 3. A plant for producing solid urea ingranule form, operating using a method according to claim
 1. 4. Thesolid urea in granule form, free from formaldehyde, obtained with amethod according to claim
 1. 5. A method for revamping a plant forproducing solid urea, wherein the plant comprised a prilling section forproduction of solid urea by means of prilling of a high-concentrationurea melt, the method comprising the steps of: installing a granulationsection and feeding at least part of said urea melt originally intendedfor the prilling section, and without the addition of formaldehyde, tosaid new granulation section.
 6. The method according to claim 5,wherein a portion of said urea melt is used in the prilling section toproduce seeds for said new granulation section.
 7. The method accordingto claim 1, wherein said urea melt has a concentration of at least 99.7%by weight.